US4689157A - Method of and device for centrifugally purifying used mineral oils - Google Patents

Method of and device for centrifugally purifying used mineral oils Download PDF

Info

Publication number
US4689157A
US4689157A US06/873,653 US87365386A US4689157A US 4689157 A US4689157 A US 4689157A US 87365386 A US87365386 A US 87365386A US 4689157 A US4689157 A US 4689157A
Authority
US
United States
Prior art keywords
run
valve
water
liquid
circulation
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
US06/873,653
Inventor
Aloys Tenthoff
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
GEA Mechanical Equipment GmbH
Original Assignee
Westfalia Separator GmbH
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Westfalia Separator GmbH filed Critical Westfalia Separator GmbH
Assigned to WESTFALIA SEPARATOR AG reassignment WESTFALIA SEPARATOR AG ASSIGNMENT OF ASSIGNORS INTEREST. Assignors: TENTHOFF, ALOYS
Application granted granted Critical
Publication of US4689157A publication Critical patent/US4689157A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Images

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B04CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
    • B04BCENTRIFUGES
    • B04B1/00Centrifuges with rotary bowls provided with solid jackets for separating predominantly liquid mixtures with or without solid particles
    • B04B1/10Centrifuges with rotary bowls provided with solid jackets for separating predominantly liquid mixtures with or without solid particles with discharging outlets in the plane of the maximum diameter of the bowl
    • B04B1/14Centrifuges with rotary bowls provided with solid jackets for separating predominantly liquid mixtures with or without solid particles with discharging outlets in the plane of the maximum diameter of the bowl with periodical discharge
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10MLUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M175/00Working-up used lubricants to recover useful products ; Cleaning
    • C10M175/0058Working-up used lubricants to recover useful products ; Cleaning by filtration and centrifugation processes; apparatus therefor

Abstract

The method is carried out with a self-emptying separator. Used mineral oil is supplied to its centrifuge drum through a central intake. Purified oil is extracted through a run-off. The separator also has another run-off for liquid extracted from the periphery of the drum. The second run-off is supplied from a sampler. A sensor is positioned in the second run-off. The sensor determines the consistency of the liquid. Downstream of the sensor is a water run-off valve. A line branches off between the sensor and the water run-off valve. The line is provided with a circulation-system valve and empties into the intake. When the circulation-system valve is open and the sensor determines from the consistency of the liquid flowing through the second run-off that the liquid is an emulsion of oil and water, it supplies the result to controls. The controls then close the circulation-system valve for a prescribed amount of time. Determination of the consistency of the liquid in the second run-off is continued at prescribed intervals of time by briefly opening the circulation-system valve until the liquid is determined to consist strictly of water. The circulation-system valve is then closed and the water run-off valve opened and kept open until the sensor determines a change in the consistency of the liquid.

Description

BACKGROUND OF THE INVENTION
The present invention relates to a method of centrifugally purifying used mineral oils, especially heavy oils contaminated with particles of dirt and slight amounts of water, by means of a self-emptying separator, with the mixture of solids and liquids being supplied to the separator's centrifuge drum through a central intake and with the purified oil being extracted from its center through a run-off, the separator also having another run-off supplied from a sampler for liquid extracted from the periphery of the drum, with a sensor positioned in the second run-off to determine the consistency of the fluid and with a water run-off valve downstream of the sensor, the liquid being returned to the intake when the water run-off valve is closed.
A method and device of this type are known from German OS No. 3 314 859. The sampler is the known device operates continuously and the liquid extracted from the periphery of the drum and supplied to the second run-off is either returned to the central drum intake or, if a sensor so determines, detoured out of the circulation system through a three-way valve.
As separation commences, oil flows into the second run-off through the run-off channel for the liquid extracted from the periphery of the drum and water accumulates in the drum's solids space. During this phase of the operation the three-way valve is positioned to return the oil to the drum's central intake. As soon as the water accumulated in the solids space arrives at the run-off channel, it is extracted through the channel and through the sampler and supplied to the second run-off. When the sensor, which can be an instrument that measures the electric conductivity of the liquid, determines that water instead of oil is flowing through the second run-off, the three-way valve is repositioned and the water is supplied to a catch point.
It has turned out in practice that a stable water phase cannot be extracted through the second run-off in accordance with the known method because the proportion of water in the intake into the drum is much lower than the run-off capacity of the amount of liquid extracted from the periphery of the drum. Thus, oil is also extracted along with the water, and both components emulsify, preventing separate diversion of the water phase. Emulsification is also promoted because the specific weights of oil and water differ so slightly and because liquid is constantly being extracted from the periphery of the drum through the sampler.
SUMMARY OF THE INVENTION
The object of the present invention is to improve a method of the aforesaid type to the extent that only water is extracted from the separator through the open water run-off valve and both the purified oil and the emulsion of oil and water that flow through the second run-off are returned to the central intake of the drum.
This object is attained in a method of the aforesaid type through an improvement wherein a line equipped with a circulation-system valve and emptying into the intake branches off between the sensor and the water run-off valve, the circulation-system valve and the water run-off valve are activated by controls, and the water run-off valve is closed when the circulation-system valve is open, wherein, as soon as the sensor determines from the consistency of the liquid flowing through the second run-off while the circulation-system valve is open that the liquid is an emulsion of oil and water, and transmits the result to the controls, the controls close the circulation-system valve for a prescribed length of time and the sensor continues to determine the consistency of the liquid in the second run-off at prescribed intervals of time with the circulation-system valve being opened briefly until the liquid is determined to be nothing but water, and wherein the controls then close the circulation-system valve and open the water run-off valve until the sensor determines a change in the consistency of the liquid, at which point the controls close the water run-off valve again and open the circulation-system valve at brief intervals to allow the sensor to carry out measurements at prescribed intervals.
In one practical embodiment of the method in accordance with the invention the circulation-system valve is opened while the water run-off valve is closed only for a limited time even during the stage of operation of the separator in which purified oil is being extracted through the second run-off, and sampling is continued at prescribed intervals of time.
The method in accordance with the invention is intermittent. The operating phases in which either the circulation-system valve or the water run-off valve is open alternate with phase in which both valves are closed. Since liquid is extracted from the periphery of the drum only at prescribed intervals of time, enough water to extract can accumulate in the drum, and the water level can shift radially inward in relation to the run-off channel. Since the sensor will detect only water during the following sampling process, the controls will open the water run-off valve and keep it open as long as pure water continues to run off, until, that is, the water level in the drum drops back to the level of the run-off in the drum. The water run-off valve is then closed and discontinuous liquid extraction recommenced.
In one preferred embodiment of the method, the circulation-system valve is kept open 15 seconds at a time and samples are obtained at intervals of 60 seconds.
The invention also relates to a device for carrying out the method, with a sensor that has a flow channel and measures the electric conductivity of the liquid, through an improvement wherein two bolt-shaped electrodes are positioned in the flow channel apart from and laterally displaced from each other in relation to the central axis of the channel.
The device can have a metal housing with a cylindrical chamber that accommodates a plastic casting that the flow channel extends through and that the electrodes are secured in.
The cross-section of the plastic casting in this embodiment can be a segment of a circle, the electrodes can be screws with their heads positioned outside a flattening and with the cable brackets for the electric connections secured in the vicinity of the heads, and the section of the chamber inside the housing that is demarcated by the flattening can be filled with plastic resin.
The device can also have at least one calibrated bore that determines how much liquid runs off and that is located in a sampler-chamber cover below the sampler.
The bores can have an inside thread, and one or more bores can be capable of being blocked off with a plug with an outside thread.
Some preferred embodiments of the invention will now be described with reference to the attached drawings, wherein
BRIEF DESCRIPTION OF THE DRAWINGS
FIG. 1 is a vertical section through a clarifier-separator with associated controls,
FIG. 2 is a longitudinal section through a sensor in the form of a conductimeter positioned in the second run-off, and
FIG. 3 is a section along the line III--III in FIG. 2.
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS
As shown in FIG. 1, a separator has a centrifuge drum 1 that is supplied with a mxiture of solids and liquid, heavy oils contaminated with particles of dirt and slight amounts of water for instance, through a central intake 2. From intake 2 the mixture arrives in a centrifuging space 3 composed of a separation space 4 and a solids space 5. Purified oil is extracted from the center of the drum over a peeling disk 6 and through a run-off 7. The liquid, which can be oil, water, or an emulsion of these two liquid components, is extracted from the periphery of the drum in the illustrated embodiment through at least one bore 8 in a parting plate 9 located in the vicinity of the inside of drum cover 10 and constituting in conjunction with the cover an annular channel 11. From annular channel 11 the liquid flows through a channel 12, a bore 13, and a calibrated bore 14 that is positioned inside a sampler-chamber cover 15 and determines how much of the liquid can run off. Above sampler-chamber cover 15 is a sampler 17 that is provided with a peeling disk 16 and that the liquid flows through into another run-off 18.
Bore 8 constitutes the beginning and bore 14 the end of the channel that the liquid extracted from the periphery of the drum runs off through inside the drum. Sampler-chamber cover 15 can have several calibrated bores, each threaded so that they can easily be blocked off with a threaded plug, making it possible to vary how much liquid runs off. This is especially practical when the drum is used to separate other types of material.
Parting plate 9 can also have several bores 8 that can be blocked off with a plug so that the drum can easily be adapted for separating other types of material.
There is a sensor 19 in second run-off 18 that determines the consistency of the liquid flowing through the run-off. The results are supplied to controls 20 that open and close a circulation-system valve 21 and a water run-off valve 22. Circulation-system valve 21 is positioned in a line 23 that branches off from second run-off 18 between sensor 19 and water run-off valve 22 and empties into central intake 2. The water flows from water run-off valve 22 into a water-accumulation reservoir 39 through another line 24.
The sensor 19 in the illustrated embodiment is a device that measures the electric conductivity of the liquid flowing through second run-off 18. The specifics of the design of this device will be evident from FIGS. 2 and 3. The device has a metal housing 25 equipped with a cylindrical chamber that accommodates a plastic casting 26. Casting 26 has a channel 27 for the liquid with the electric conductivity that is to be measured to flow through. To determine the conductivity the device has two bolt- shaped electrodes 28 and 29. Electrodes 28 and 29 are separated and laterally displaced in relation to the central axis 30 of flow channel 27.
Electrodes 28 and 29 are screws. Cable brackets 32 for the electric-connection lines are secured in the vicinity of the heads 31 of the screws. The cross-section of plastic casting 26 is a segment of a circle and has a flattening 33. Screw heads 31 and cable brackets 32 are positioned below flattening 33. The section of the chamber that accommodates flow channel 27 in housing 25 that is demarcated by flattening 33 and that is not occupied by casting 26 is filled with plastic resin, epoxide resin for example. Housing 25 has a flange 34, to which a terminal disk 36 is secured with screws 35. The channel 27 that the liquid with the conductivity that is to be measured flows through also extends through terminal disk 36 and through the wall of the channel that faces it.
This type of conductimeter is simple in design and allows for a small flow cross-section that no deposits can occur in.
Controls 20 can be set to carry out samplings by extracting liquid from the periphery of the drum through second run-off 18 at intervals of 60 seconds while the separator is in operation and to keep circulation-system valve 21 open 15 seconds at a time.
As soon as the water level in drum 1 reaches the bore 8 in parting plate 9, an emulsion of water and oil will flow through second run-off 18 during the next sampling and will be conveyed into central intake 2 through circulation-system valve 21 and line 23, with water run-off valve 22 closed. Once circulation-system valve 21 has been open for 15 seconds, it will close again and remain closed for 60 seconds, allowing water to accumulate in drum 1 again, so that the water level can shift radially in in relation to bore 8. During the next sampling pure water will flow through second run-off 18, and controls 20 will close circulation-system valve 21 and open water run-off valve 22, keeping it open until sensor 19 detects a change in the consistency of the liquid, sensing an emulsion of water and oil.
The solids space 5 of the drum 1 illstrated in FIG. 1 has expulsion apertures 37 around it that can be blocked off and released by an axially moving piston slide 38.
It will be appreciated that the instant specification and claims are set forth by way of illustration and not limitation, and that various modifications and changes may be made without departing from the spirit and scope of the present invention.

Claims (3)

What is claimed is:
1. In a method of centrifugally purifying used mineral oils comprising a mixture of oil contaminated with particles of dirt and slight amounts of water, by supplying the mixture of solids and liquids to a centrifuge drum of a self-emptying separator through a central intake, extracting the purified oil from the center of the drum through a run-off, extracting liquid from the periphery of the drum via a sampler through a second run-off with a sensor positioned in the second run-off to determine the consistency of the liquid and with a water run-off valve downstream of the sensor and returning liquid to the intake when the water run-off valve is closed, the improvement comprising: disposing a circulation-system valve in a line emptying into the intake and branching off between the sensor and the water run-off valve, closing the water run-off valve when the circulation-system valve is open, to enable the sensor to determine from the consistency of the liquid flowing through the second run-off while the circulation-system valve is open if the liquid is an emulsion of oil and water, closing the circulation-system valve for a prescribed length of time when an emulsion of oil and water is sensed and enabling the sensor to continue to determine the consistency of the liquid in the second run-off at prescribed intervals of time by briefly opening the circulation-system valve until the liquid is determined to be nothing but water, and closing the circulation-system valve and opening the water run-off valve until the sensor determines a change in the consistency of the liquid, and thereafter closing the water run-off valve again and opening the circulation-system valve at brief intervals to allow the sensor to carry out measurements at prescribed intervals.
2. The method as in claim 1, wherein the circulation-system valve is opened while the water run-off valve is closed only for a limited time even when purified oil is being extracted through the second run-off, and sampling is continued at prescribed intervals of time.
3. The method as in claim 1, wherein the circulation-system valve is kept open 15 seconds at a time and samples are obtained at intervals of 60 seconds.
US06/873,653 1985-07-04 1986-06-12 Method of and device for centrifugally purifying used mineral oils Expired - Lifetime US4689157A (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DE3523907 1985-07-04
DE3523907A DE3523907A1 (en) 1985-07-04 1985-07-04 METHOD AND DEVICE FOR CENTRIFUGAL CLEANING OF USED MINERAL OILS

Publications (1)

Publication Number Publication Date
US4689157A true US4689157A (en) 1987-08-25

Family

ID=6274930

Family Applications (1)

Application Number Title Priority Date Filing Date
US06/873,653 Expired - Lifetime US4689157A (en) 1985-07-04 1986-06-12 Method of and device for centrifugally purifying used mineral oils

Country Status (8)

Country Link
US (1) US4689157A (en)
JP (1) JPH0742464B2 (en)
BR (1) BR8603089A (en)
DE (1) DE3523907A1 (en)
ES (2) ES8707758A1 (en)
FR (1) FR2584415B1 (en)
IT (1) IT1189759B (en)
SE (1) SE464969B (en)

Cited By (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4840612A (en) * 1987-06-24 1989-06-20 Alfa-Laval Marine And Power Engineering Ab Centrifugal separator and method of operating same
US4900453A (en) * 1987-08-07 1990-02-13 Krause-Maffei Aktiengesellschaft Filter centrifuge control
US4990265A (en) * 1988-08-30 1991-02-05 Westfalia Separator Ag Method of dewatering oil mud
EP0438235A2 (en) * 1990-01-16 1991-07-24 W.R. Grace & Co.-Conn. Directional diffusion nozzle air bar
WO2000053330A1 (en) * 1999-03-09 2000-09-14 Alfa Laval Ab Centrifugal separator with inlet chamber and outlet chamber centrally located in the rotor
WO2005065835A1 (en) * 2003-12-23 2005-07-21 Westfalia Separator Ag Method and device for preventing blockages in the flow paths of a separator
US20060000787A1 (en) * 2004-07-02 2006-01-05 Galasso Louis Iii Purification of impure oil by centrifugation
US20080017595A1 (en) * 2004-07-21 2008-01-24 Karl-Heinz Zettier Separator And Method For Disinfecting Raw Milk Or Whey
US20110189359A1 (en) * 2008-10-13 2011-08-04 Gea Mechanical Equipment Gmgh Method for reducing the pulp content of fruit juices containing pulp
US20130065744A1 (en) * 2010-03-19 2013-03-14 Per Karlsson Device and method for monitoring and adjusting the radial position of an interface layer in a nozzle centrifuge
US20150051059A1 (en) * 2012-03-26 2015-02-19 Gea Mechanical Equipment Gmbh Separator Arrangement
US10046336B2 (en) 2015-06-10 2018-08-14 Alfa Laval Corporate Ab Scrubber fluid treatment process

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH04504677A (en) * 1989-04-24 1992-08-20 ヘンケル・コマンディットゲゼルシャフト・アウフ・アクチェン Auxiliary equipment for separator
DE19528021C1 (en) * 1995-07-31 1996-11-07 Karl Donnert Centrifugal oil-water separator esp. suitable for dealing with bulk tanker accidents
DE19700753C2 (en) * 1997-01-11 2000-09-14 Schott Glas Hob with a non-metallic hotplate
JP6177835B2 (en) * 2015-06-25 2017-08-09 アルファ・ラバル・コーポレイト・エービー Scrubber liquid treatment process

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3642196A (en) * 1969-05-08 1972-02-15 Alfa Laval Ab Centrifuge with sludge level sensing means
US4325825A (en) * 1979-04-26 1982-04-20 Hoechst Aktiengesellschaft Separator

Family Cites Families (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1318086A (en) * 1919-10-07 And keclaimistg system
US1778831A (en) * 1924-04-29 1930-10-21 Sharples Specialty Co Oil-purifying process
GB279636A (en) * 1926-10-29 1927-11-03 Nevin E Funk Improvements relating to the treatment of lubricating oils
GB409522A (en) * 1933-06-12 1934-05-03 Cornelis Van Grondelle Process of preparing purified lubricating and electrical resistance oil from used or waste oils
DE678318C (en) * 1937-06-01 1939-07-13 Bergedorfer Eisenwerk Akt Ges Liquid discharge device in a centrifugal separator
US3261546A (en) * 1962-10-29 1966-07-19 Pfaudler Permutit Inc Method for clarifying fats and oils
US3265212A (en) * 1963-05-09 1966-08-09 Pennsalt Chemicals Corp Process for the purification of rolling mill oil
US3835035A (en) * 1973-07-30 1974-09-10 Auley C Mc Method of purifying lubricating oils
DE2438602B2 (en) * 1974-08-10 1976-09-16 Alfa Laval Industrietechnik Gmbh, 2056 Glinde DEVICE FOR SEPARATION OF SOLIDS AND WATER FROM OLD ELECTRIC Sludge
US4033859A (en) * 1975-04-24 1977-07-05 Witco Chemical Corporation Thermal treatment of used petroleum oils
GB2038868B (en) * 1979-11-12 1982-09-22 Waste Lubricating Oils Ltd Method and apparatus for reprocessing waste oils
SE8302215D0 (en) * 1983-04-20 1983-04-20 Alfa Laval Marine Power Eng centrifugal
DE3314859A1 (en) * 1983-04-23 1984-10-25 Westfalia Separator Ag, 4740 Oelde METHOD AND DEVICE FOR CENTRIFUGAL CLEANING OF USED MINERAL OILS

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3642196A (en) * 1969-05-08 1972-02-15 Alfa Laval Ab Centrifuge with sludge level sensing means
US4325825A (en) * 1979-04-26 1982-04-20 Hoechst Aktiengesellschaft Separator

Cited By (19)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4840612A (en) * 1987-06-24 1989-06-20 Alfa-Laval Marine And Power Engineering Ab Centrifugal separator and method of operating same
US4900453A (en) * 1987-08-07 1990-02-13 Krause-Maffei Aktiengesellschaft Filter centrifuge control
US4990265A (en) * 1988-08-30 1991-02-05 Westfalia Separator Ag Method of dewatering oil mud
EP0438235A2 (en) * 1990-01-16 1991-07-24 W.R. Grace & Co.-Conn. Directional diffusion nozzle air bar
EP0438235B1 (en) * 1990-01-16 1995-03-15 W.R. Grace & Co.-Conn. Directional diffusion nozzle air bar
WO2000053330A1 (en) * 1999-03-09 2000-09-14 Alfa Laval Ab Centrifugal separator with inlet chamber and outlet chamber centrally located in the rotor
US20070082802A1 (en) * 2003-12-23 2007-04-12 Siegfried Klapper Method and device for preventing blockages in the flow paths of a separator
WO2005065835A1 (en) * 2003-12-23 2005-07-21 Westfalia Separator Ag Method and device for preventing blockages in the flow paths of a separator
US7837608B2 (en) * 2003-12-23 2010-11-23 Westfalia Separator Ag Method and device for preventing blockages in the flow paths of a separator
US20060000787A1 (en) * 2004-07-02 2006-01-05 Galasso Louis Iii Purification of impure oil by centrifugation
US20080017595A1 (en) * 2004-07-21 2008-01-24 Karl-Heinz Zettier Separator And Method For Disinfecting Raw Milk Or Whey
US7758488B2 (en) * 2004-07-21 2010-07-20 West falia Separator AG Method of operating a separator by recirculating an entraining liquid
US20110189359A1 (en) * 2008-10-13 2011-08-04 Gea Mechanical Equipment Gmgh Method for reducing the pulp content of fruit juices containing pulp
US8557316B2 (en) * 2008-10-13 2013-10-15 Gea Mechanical Equipment Gmbh Method for reducing the pulp content of fruit juices containing pulp
US20130065744A1 (en) * 2010-03-19 2013-03-14 Per Karlsson Device and method for monitoring and adjusting the radial position of an interface layer in a nozzle centrifuge
US8702576B2 (en) * 2010-03-19 2014-04-22 Alfa Laval Corporate Ab Device and method for monitoring and adjusting the radial position of an interface layer in a nozzle centrifuge
US20150051059A1 (en) * 2012-03-26 2015-02-19 Gea Mechanical Equipment Gmbh Separator Arrangement
US10105717B2 (en) * 2012-03-26 2018-10-23 Gea Mechanical Equipment Gmbh Method for operating a separator with a drive chamber under negative pressure
US10046336B2 (en) 2015-06-10 2018-08-14 Alfa Laval Corporate Ab Scrubber fluid treatment process

Also Published As

Publication number Publication date
SE8602947L (en) 1987-01-05
JPH0742464B2 (en) 1995-05-10
FR2584415A1 (en) 1987-01-09
ES8707758A1 (en) 1987-08-16
ES555447A0 (en) 1987-08-16
SE464969B (en) 1991-07-08
DE3523907C2 (en) 1992-03-19
BR8603089A (en) 1987-02-17
SE8602947D0 (en) 1986-07-02
IT1189759B (en) 1988-02-04
IT8612484A0 (en) 1986-05-28
JPS6210189A (en) 1987-01-19
DE3523907A1 (en) 1987-01-15
ES557530A0 (en) 1987-12-01
FR2584415B1 (en) 1989-11-24
ES8800848A1 (en) 1987-12-01

Similar Documents

Publication Publication Date Title
US4689157A (en) Method of and device for centrifugally purifying used mineral oils
US4525155A (en) Centrifugal separator and method of operating the same
US4755165A (en) Method and device for separating two liquid phases by means of a centrifuge
JP2596591B2 (en) How to operate the centrifuge
SU577946A3 (en) Centrifugal separator
US6358193B1 (en) Regulation device for a centrifugal separator to control discharge from outlets
EP0205246B1 (en) Centrifugal separator
US4151950A (en) Continuously operating centrifugal separator having hydraulically operated valves
US3750940A (en) Control means for self-discharging centrifuge
US5800330A (en) Method and equipment for monitoring a centrifugal separator
CA2298826C (en) Apparatus and method for separating a mixture of a less dense liquid and a more dense liquid
FR2592324A1 (en) VORTEX ROTATING SEPARATOR FOR HETEROGENEOUS LIQUID.
JPS60153960A (en) Centrifugal separation apparatus
FR2446678A1 (en) CENTRIFUGAL SEPARATOR
JPS6036010B2 (en) Composition analyzer
US4149668A (en) Centrifugal separator with outlet valves
US2723799A (en) Centrifugal separation
JP4397516B2 (en) Separator plate centrifuge and method for operating the same
US3976242A (en) Self-emptying clarifying separator having a foam-free removal of the clarified liquid by means of a paring disk and an automatically operating system for detecting the level of the solids in the sludge chamber
JPS63305953A (en) Automatic discharge type centrifugal drum
JPS63252560A (en) Centrifugal separator
GB2139121A (en) Centrifugal cleaning of used mineral oils
SE461019B (en) CENTRIFUGAL SEPARATOR WITH A PUMP BODY, ESTABLISHED TO ACHIEVE A CIRCULATION OF LIQUID IN A CIRCULATION CIRCUIT
RU2125490C1 (en) Centrifugal liquid cleaner
CS245672B1 (en) Method and apparatus for automaticseparation of two or more unmixable liquid phases

Legal Events

Date Code Title Description
AS Assignment

Owner name: WESTFALIA SEPARATOR AG, WERNER-HABIG-STRASSE 1 474

Free format text: ASSIGNMENT OF ASSIGNORS INTEREST.;ASSIGNOR:TENTHOFF, ALOYS;REEL/FRAME:004564/0221

Effective date: 19860605

STCF Information on status: patent grant

Free format text: PATENTED CASE

CC Certificate of correction
FEPP Fee payment procedure

Free format text: PAYOR NUMBER ASSIGNED (ORIGINAL EVENT CODE: ASPN); ENTITY STATUS OF PATENT OWNER: LARGE ENTITY

FPAY Fee payment

Year of fee payment: 4

FPAY Fee payment

Year of fee payment: 8

FEPP Fee payment procedure

Free format text: PAYOR NUMBER ASSIGNED (ORIGINAL EVENT CODE: ASPN); ENTITY STATUS OF PATENT OWNER: LARGE ENTITY

Free format text: PAYER NUMBER DE-ASSIGNED (ORIGINAL EVENT CODE: RMPN); ENTITY STATUS OF PATENT OWNER: LARGE ENTITY

FPAY Fee payment

Year of fee payment: 12

FEPP Fee payment procedure

Free format text: PAYOR NUMBER ASSIGNED (ORIGINAL EVENT CODE: ASPN); ENTITY STATUS OF PATENT OWNER: LARGE ENTITY

Free format text: PAYER NUMBER DE-ASSIGNED (ORIGINAL EVENT CODE: RMPN); ENTITY STATUS OF PATENT OWNER: LARGE ENTITY